Animal feed supplement

ABSTRACT

The invention provides a highly nutritional unfermented medium protein animal feed supplement by admixing wet corn bran having an abnormally high moisture content with concentrated corn steep to form a moist cohesive but friable mass, the process elminating a significant proportion of the energy used in and pollution occasioned by prior art process. In a modification, the above unfermented product is subjected to a natural fermentation stage resulting in a fermented supplement which is microbiologically and gravitationally stable for an extended period of time. One further advantage of the present invention is that the corn bran and steep liquor from a corn wet milling plant can be used in the specific amounts as actually produced in the normal operation of the plant, thereby allowing plant efficiencies to be maintained.

This is a continuation-in-part of U.S. Ser. No. 222,029 filed Jan. 2,1981, now abandoned.

This invention relates to animal feed supplements derived fromindustrial by-products and in particular, the wet corn milling industry.

BACKGROUND OF THE INVENTION

Many industrial processes produce a variety of by-products which havesignificant potential forms as an animal feed or animal feed supplement.For example, the alcoholic brewing industry produces spent yeast as aby-product, this material containing a relatively larger portion ofproteinaceous nitrogen and some vitamins, especially vitamin B andconsequently the product is used as a protein supplement in animalfeeds. Refer, for example, to Applicant's U.S. Pat. No. 4,055,667 andalso Canadian Pat. No. 959,332. In addition, the second major by-productof the brewing industry, namely spent brewers' grains, is alsoutilizable as an animal feed--refer for example to U.S. Pat. No.3,875,304. A further industry which produces a large volume ofby-products also utilizable as animal feeds is the wet corn millingindustry, the two major by-products being corn steep water and wet cornbran. The former comprises the condensed corn extractives "steep liquoror water" resulting from the wet milling manufacture of corn starch orsyrup which are collected and condensed generally to about 50% solids byevaporation. All of the soluble nutrients in corn grain (for exampledissolved vitamins, minerals and other solubles or dispersiblenutrients) are contained in the steep water. The corn steep water ishandled and stored in tanks and treated in a manner similar to otherliquid feed ingredients. The corn steep water is an economical source ofprotein being equivalent on a dry basis to 44% soybean meal. It is alsoan excellent source of energy and phosphorus and the dissolved nutrientsfrom the corn which, if not, as is usual, reduced in availability boundto subsequent process steps, would be readily available to the animals.A typical proximate analysis of corn steepwater is as follows:

    ______________________________________                                                 Crude                                                                         Protein                                                                              Fat    Fibre   Ca    P    ASH                                 ______________________________________                                        50% Dry Matter                                                                           22.5%    0      0     0.1%  0.6% 3.9%                              ______________________________________                                    

and more detailed analyses are readily available in the literature. Itmay be noted that corn steep liquor per se is quite stablemicrobiologically and consequently presents no real problems on thataccount during storage. Wet corn bran comprises that part of thecommercial shelled corn remaining after the extraction of the largerportion of starch, gluten and germ by the processes employed in the wetmilling manufacture of the corn starch or syrup prior to drying. (Itdoes not, of course, include the extractives i.e. steep water, refer toabove.) The product constitutes the corn kernels hull and fibrousparticles, and, when utilized alone, may contain an organic acid forextending its shelf life, since the product is extremely prone tomicrobial degradation. It has a high propensity to heating resulting insignificant mold growth within a short period of time, even abouttwenty-four hours or so, depending on storage conditions. Wet corn branas exiting the wet corn wet milling process contains 65% moisture andthis is usually reduced to about 10% by drying and it can then be usedfor feed in that condition. A typical analysis of wet corn bran is asfollows:

    ______________________________________                                                 Crude                                                                         Protein                                                                              Fat    Fibre   Ca    P    Ash                                 ______________________________________                                        100% Dry Matter                                                                          11.5%    5.0%   10.0% 0.05% 0.20%                                                                              2.2%                              ______________________________________                                    

For a short term feeding of wet corn bran containing an organic acidpreservative, a pit silo, a cement slab or a simply constructed woodenbox is quite satisfactory to contain the product. Protection from theelements, particularly heavy rains, is highly desirable since thepreserving acid may be leached out resulting in the product beingsubject to spoilage. Wet corn bran is mainly an economic source ofenergy in ruminant rations but also contributes about 11% protein on adry matter basis. Both wet corn bran and corn steep liquor haverelatively low solid contents, about 35% and 50% respectively, in thestate they usually exit the milling process and are not easily orconveniently utilized in that form. In particular, such corn steepliquor when used as an ingredient in traditional liquid feed supplementsis subject to re-crystalization and other handling problems. On theother hand bran fibre at the 35% d.m. solids level has a low bulkdensity and does not compact well with the result that the mass ofmaterial is generally air-permeable and/or develops air pockets; the netresult in both instances being rapid mold growth. Consequently, in manyoperations, the wet corn bran, having a moisture content of about 65%,is dried to a moisture content generally below 20% and is then mixedwith the corn steep liquor having a moisture content of about 50% andthe resulting mixture is dried, in a flash drier or in a steam tubedrier, to a moisture content of at most about 10%. This dried product isthen sold as an animal feed supplement having a protein content of about20%. (If corn bran per se is sold as a feed component it too is dried toa moisture content of less then 10% for the same reasons) However, thatsystem has many disadvantages including the following:

1. The expenditure of a large amount of energy in drying the variouscomponents and the resulting product.

2. There may be extensive heat denaturation of the nutrients in theresulting product.

3. Valuable heat volatile and/or fine particulate nutrients in the mixbeing dried are lost by evaporation.

4. The importance of viable Lactobacillus in warm-blooded animals inhelping to maintain the proper balance of intestine flora has beendocumented and, indeed, viable Lactobacillus is sold as a feedsupplement for use in appropriate situations. Drying of the productsubstantially eliminates the Lactobacillus viability thereby removingany possibility of the animals taking advantage of a potential valuabledietary component;

5. There is relatively large capital investment and costly maintenancein the drying equipment required.

6. Operation of the drying equipment results in a pollution problemcomprising mainly particulate emissions and very undesirable odouremissions.

7. As in all such wet milling operations, if the drier for the animalfeed product becomes inoperative, the whole milling process is beensubject to shut-down.

Many ways of utilizing the by-products of the wet corn milling industry,and indeed, the wet wheat milling industry, have been proposed but, toApplicant's best knowledge, all leave a lot to be desired and allgenerally suffer from one or more of the above disadvantages. A majorfeature of the prior proposals is that the animal feed product isrequired to be dried to a relatively low moisture content immediatelyfollowing its production. Refer for example to U.S. Pat. No. 4,181,748which discloses a continuous process for refining whole grain corn. Thiscomplex process utilizes both a dry milling stage and a wet millingstage, this presumedly, requiring two complete mills since thetheoretically possible sequential treatment route would result in abatch operation while the process is stated to be continuous. Moreover,the wet milling stage involves two steeping steps. Various fractionsfrom both the dry milling and wet milling stages are combined to form awet animal feed composite which, in the usual manner, is dried over aperiod of hours to form the desired animal feed product. In U.S. Pat.No. 4,171,353, there is disclosed a wet milling process for refiningwhole grain wheat, in which process again two steeping steps are usedand a variety of product streams from the multistage process arecombined to form a wet animal feed composite. The composite is then, inthe usual manner, dried to a moisture content of from 10-12% by heatingat elevated temperatures. A significant claim for this process is thatall of the milling is wet milling to avoid damage to the substrate.Other known processes which suffer from similar disadvantages aredescribed in U.S. Pat. Nos. 4,171,383 and 4,171,384. In summary, priorart attempts to use the by-products of wet milling processes havegenerally required changes to be made to the basic wet milling operationand/or have used a combination of wet and dry milling stages: however,the common feature associated with the various processes is that any wetanimal feed composite resulting from such processes are required to bedried immediately, this merely reflecting the widely held industry viewthat such materials when wet would, invariably, be subject to spoilagewithin a very short time.

It is an object of the present invention to provide animal feedsupplements which, from a practical viewpoint, are in, at most, a moistform, from the wet corn bran and corn steep liquor by-producs of a wetcorn milling process, which products are gravitationally andmicrobiogically stable.

A further object of the present invention is a process for theproduction of an animal feed supplement from wet corn bran and steepliquor which process is able to utilize those components and especiallythe wet corn bran in the quantities they are normally produced in anytypical wet corn milling plant, the routine operation, and consequentlyefficiency, of which need not therefore be disrupted.

GENERAL STATEMENT OF INVENTION

It has now been found, and this finding forms the basis of the presentinvention, that corn steep liquor from a wet corn milling process hasthe ability when admixed with wet corn bran from the same process, topreserve the corn bran and thereby produce a valuable unfermented animalfeed supplement having good keeping qualities.

A further major feature of the invention is that the corn bran asadmixed with the steep liquor has a high moisture content--the watercontent of the bran exiting the usual corn wet-milling process isreduced to only an intermediate level prior to it being admixed--as doesthe feed produced, and this results in several major advantagesincluding, for example, a significant energy saving in its production.

In a further aspect of the invention the product as formed above issubjected to an anaerobic fermentation stage during which the materialis converted, without further drying, into a moist friable mass. Theproduct is gravitationally and microbially stable and is anon-agglomerating mixture having no obvious undesirable "wetcharacteristics" in spite of the fact that it still has a substantialmoisture content of 50% or more by weight. Under normal conditions,there is no tendency for the feed component particles or the like eitherduring the formation of the friable mass or subsequently followingseparation or division into smaller amounts, to stick or fuse togetherto form undesirable large indurated lumps and it is relatively easy todivide the mass as required. Consequently, the product may be readilytransported via conventional transfer systems from its storage locationto place of consumption. This ability of the mass of product produced byfermentation to be readily divided is described herein as its ability tobe "readily reduced to a non-agglomerating product".

All animal feeds, whether fluid feeds or non-pelleted "solid" feeds areprone to component separation especially during distribution and, in thecase of high moisture products as are the present products, duringstorage, this being caused at least in part because of the influence ofgravity. In fluid feeds suspended solids tend to precipitate out and insolid feeds liquid components may separate from solid components andvarious solid components because, for example, of differing particlesizes may separate i.e. particles of the same general size (and usuallysame type of material) may come together. Such separation is obviouslyhighly undesirable and an animal feed is said to be "gravitationallystable" if it has the ability to substantially resist such componentseparation during distribution and for an extended period of time and atleast the projected life of the product; in this case at least severalweeks but usually much longer.

DETAILED STATEMENT OF INVENTION

In one aspect, the present invention provides a process for producing amicrobiologically stable unfermented animal feed supplement from cornsteep liquor and wet corn bran exiting a wet corn milling process,comprising:

(a) mechanically dewatering the wet corn bran to a solids content offrom 20% to 50% by weight;

(b) thoroughly admixing the de-watered bran with concentrated corn steepliquor having a solids content of from to preferably 45% to 55% byweight in the ratio of de-watered corn bran: steep liquor of from 3:1 to1:2 with the resulting mixture having a solids content of from 35% to50% by weight

(c) compacting the resulting mixture to form a moist cohesive masshaving a bulk density of from 50, preferably 55, to 65 lb/cuft, a pH ofless than 4.5 and a protein content of at least 20% on a dry matterbasis of the solids content.

The steep liquor: bran ratio is extremely important, if too low i.e. theamount of steep liquor is too low, then the bran will be subject torapid deterioration as referred to above, and if too high retention ofthe liquid components with the mass will be adversely affected resultingin undesirable leaking i.e. separation at the storage location.

It has also been found that the uniquely high moisture content of thewet corn bran component greatly assists thorough mixing of the bran andsteep liquor as well as the efficient compaction of the resultingmixture. This may be compared with predried bran exiting standard cornwet milling operations which is more resistant to wetting and tends tocake during mixing with other feed materials, this leading to unevendistribution and poor steep liquor penetration resulting in inferiorkeeping qualities. The extremely poor keeping qualities of wet cornbran, per se, have already be referred to above.

It must be emphasized that these advantages are obtained with asignificant net reduction in energy compared with prior processes wheremixtures of wet corn bran and corn steep liquor are dried to a very lowmoisture content (less than 10%) prior to admixing and subsequent dryingof the resulting product.

Another advantageous feature of the above feed supplement is that itstill contains nutritional components which are usually lost when thecorn bran, and corn bran mixtures with steep liquor, etc. are dried asin prior art processes.

The above product is conveniently produced in the corn wet milling plantand trucked immediately to the customer. It may be noted that thedesired degree of compaction may be obtained, at least partially, whilethe product is being handled during its supply to the customer, i.e.during the actions involved in truck loading and carting, and unloadingand ensiling at the customer's premises. Additional compacting ifrequired can be effected by tramping, rolling or the like. The productis intended to be used relatively soon following production, within afew days in general, by customers who are supplied on a regular basiswith only relatively short time periods between deliveries.

However, in a further aspect, the present invention also provides afermented feed supplement which has extended stability and keepingqualities. In this embodiment, the inventive unfermented feedcomposition described above is subjected to a natural fermentation stageunder anaerobic conditions during which, it is converted into a friablefermented mass having a pH of less than about 4.5 which mass isgravitationally and microbially stable for a relatively extended periodof time and readily reduced to a non-agglomerating product which iseasily and conveniently handled.

The fermentation process proceeds rapidly at first and subsides as thepH level stabilizes, preferably at a value of 3.75 to 4.25. Thefermentation process has generally commenced by about the third dayfollowing compacting of the components and, practically speaking,fermentation may be considered complete by about the seventh day. Theresulting product will keep for prolonged periods of time provided it isundisturbed and extraction of portions thereof is effected using normalensiling methods.

As will be appreciated the fact that the unfermented product can readilybe converted into the fermented product provides the user with a highdegree of flexibility. For example, if for some reason, a delivery ofthe unfermented feed supplement cannot be used as early as expected thenit can be converted to the corresponding fermented product and no lossis incurred. Moreover, since nothing of significance nutritionally islost during the fermentation stage, the user may, without changing theration fed to his animals, begin feeding the unfermented feedcomposition and change to the fermented feed product or vice versa asdesired.

It is believed that viable Lactobacillus micro-organisms present inlarge numbers in the steep liquor, and not rendered inactive uponomitting the usual severe drying step, in combination with residualfermentable unextracted starches in the bran (which may comprise up to15% by weight on a d.m. basis) result in a fermentation stage which issimilar to a natural ensiling process yielding natural organic acidswhich lower the pH of the product and serve to enhance the preservationof the product.

It may be noted that the Lactobacillus microorganism content in both theunfermented and fermented supplements of the present invention is alwaysgreater than 1000/gm compared with counts below 50/gm for the prior artcorn bran--steep liquor co-dried material. It is pointed out that thishighly desirable component is not merely an additive in the sense thatit is separately added: its presence results directly from the inventivefeatures of the present invention.

If desired other ingredients may be incorporated into the feed productsof the present invention. For example, corn gluten meal which isnormally sold as a separate dried feed ingredient may be incorporated inthe products of the present invention and can significantly increase theprotein content of final feed mixture.

Yet a further major advantage of the present invention is that it isfully able to utilize the steep liquor and wet corn bran etc. in theamounts and ratio substantially as is normally produced in the corn wetmilling process. Therefore the only changes which are required to bemade to the corn wet milling process and plant are the elimination ofthe steps, and associated equipment, required to prior dry the wet branto a relatively low moisture level and, subsequently, extensively drythe resulting mixtures to the desired feed product. This results notonly in a significant reduction in the energy required to produce thefeed product but also leaves the beneficial lactobacillus content of thesteep liquor substantially intact; and substantially reduces oreliminates the particulate and odour pollution aspects normallyassociated with the treatment of corn wet milling by-products.

As stated above, a major feature of the present invention is the findingthat the natural keeping qualities of the corn steep liquor can be usedto preserve the readily soluble corn bran. In some instances, the amountand quality (protein content, etc.) of some instances, the amount andquality (protein content, etc.) of the corn steep liquor may be inexcess of that required to preserve the bran and to provide theresulting inventive product with the necessary protein contentrespectively. Feed products of this type are sold, mainly on the basisof their minimum protein content and increases in that protein level arenot generally economically advantageous to producer. Consequently, insome instances the amount of corn steep liquor, which provides the majorportion of starch in the product, produced may be in excess of thatrequired to be combined with all of the bran produced in the same plantfrom the stabilization and/or protein level viewpoint. In thosecircumstances any such excess corn steep liquor may be sold separately,for example, as a high protein (greater than 40% d.m. basis) feedsupplement or for other purposes. The economics of selling the steepliquor separately would depend on many factors, especially thecapability of the specific plant in question to conveniently handle theliquid steep. In such a situation, the ratio of corn bran:steep liquoractually required to produce the desired product of the presentinvention having a selected protein content can be readily calculated byusing, for example, a simple Pearson square calculation.

In this specification the term "wet corn bran" means the mixture of wetcorn bran optionally combined with corn screenings or offal and/or corngerm meal produced in a separate by-product stream, the latter beingincorporated if a high protein product is required.

A. The present invention will be further described, but not limited by,reference to the following specific descriptions of the invention ascarried out utilizing the by-products of a various corn wet millingoperation located in North America.

This plant located in Ontario, Canada, is a relatively small one whichprocesses approximately 9,500 bushels (bus.) of corn per day.Theoretically, each bushel of corn yields the following amounts ofby-products on a dry matter (d.m.) basis

corn steep liquor--3.5 lb./bu.

corn bran--5.1 lb./bu.

The theoretical crude protein on a lb. (d.m. basis)/bus. isapproximately 2.15 lbs and consequently comprises 25% of the dry mattercontained in the bran and steep when combined.

These by-products were, of course, obtained in the wet state. The cornsteep liquor was concentrated in the usual manner and the wet corn branstream concentrated mechanically by treatment in a press and acentrifuge: the two components then had the following dry matter (d.m.)compositions:

    ______________________________________                                                  (a) Dry Matter                                                                          (b) Crude Protein                                         ______________________________________                                        corn steep  48%         44% of (a)                                            corn bran   38%         12% of (a)                                            ______________________________________                                    

(The moisture content of the so-concentrated wet corn bran, namely 62%,may be compared with that of the prior art dried corn bran productscontaining less than 10%).

A batch consisting of approximately 15,545 kg was formed by mixingapproximately 10,722 kg of the wet corn bran and 4,817 kg of the cornsteep liquor in a turbolizer mixer (average residence time about 0.75minutes) and the batch introduced directly into a truck. The loadingtime, if the bran and steep were utilized as produced by the plant,would have been approximately four (4) hours but this was reduced to2.75 hours by prior filling of a surge bin with part of the wet cornbran and pumping the steep liquor from storage. The actual mixing rateswere about 143 lb./min. of the bran and slightly more than 64 lb./min.of the steep, and the ratio of concentrated corn bran:corn steep liquorwas about 2.2:1. The product was delivered immediately to a farm storagesite, some of the required compaction occuring during transit and theremainder during unloading and ensiling at the storage site. Theunfermented feed supplement was in the form of a cohesive mass havingthe following composition:

    ______________________________________                                        Dry Matter      38.58%                                                        Crude Protein   23.72%                                                        pH              4.5                                                           Bulk Density    62 lbs./cuft                                                  ______________________________________                                    

Some of this product was utilized immediately as part of the dailyration for a beef herd.

The remaining product was maintained in an undisturbed condition andunderwent a natural fermentation process which was substantiallycomplete within seven (7) days resulting in a stabilized fermentedproduct having approximately the composition of the unfermented productbut having a pH of about 4; in its undisturbed condition, the productwould remain unspoiled for an extended period of seven months or more.

Both the unfermented and fermented products according to the presentinvention were fed to the animals as a medium protein supplement andfound immediate acceptance with total success.

As in all large scale operations involving the processing of naturalproducts, there will generally be some variance in characteristics ofthe products and in particular, any by-products exiting the operation.This is true of the corn bran and steep liquor starting materials forthe process of the present invention and variances within the followinglimits are commonly obtained:

    ______________________________________                                                     (a) Dry Matter                                                                          (b) Crude Protein                                      ______________________________________                                        Concentrated Corn Bran                                                                       35-40       11-13                                              Corn Steep Liquor                                                                            45-50       43-45                                              ______________________________________                                    

Such variances, of course, could lead to variances in the crude proteincontent, etc. in the product and must be taken into account whenselecting mixing ratios of bran and steep.

The above described corn wet milling plant is capable of producing about3,800 kg/hr (8,500 lb/hr) of the unfermented product of the presentinvention at about the 40% d.m. basis.

Moreover, it may be noted that during the carrying out of the process ofthe present invention the milling plant operated substantially normally,the only significant changes concerning less than normal drying of thewet bran component and total elimination of the drying of the resultingfeed mixture.

Using the general processing conditions described above a large numberof batches comprising 15,000 to 16,000 kg (i.e. truckloads) ofunfermented product were produced. The composition of the concentratedcorn bran and the corn steep liquor starting materials fell with thevariances given immediately above and the corn bran:corn steep liquormixing ratio fell within the range of 3:1 to 1:1. As previously, theproducts as soon as they were prepared were delivered to the locationwhere they were to be used. Full analyses of the products not availablesince they are not required commercially and consequently were noteffected. However, in each instance the bulk density of the compactedproduct fell within the range of 55 to 65 lb./cuft and the Lactobacilluscount was 1000/gm

    ______________________________________                                        Batch     D.M.           C.P.   pH                                            ______________________________________                                        7804      35.75          21.65  4.0                                           7767      44.22          25.43  4.5                                           7769      37.55          24.36  4.2                                           7771      40.00          20.85  4.0                                           7556      40.25          23.04  3.9                                            014      48.31          24.8   4.1                                           7758      40.5           20.3   4.4                                           ______________________________________                                    

    ______________________________________                                        Batch D.M.    C.P.    pH  Ca   P     Fibre Fat  Ash                           ______________________________________                                        7504  40.0    26.9    --  --   --    6.3   0.09 7.37                           288  41.8    20.5    --  0.05 1.01  --    --   --                             289  39.9    23.7    --  0.09 1.33  --    --   --                            7544  37.3    22.9    --  --   --    7.32  --   --                            ______________________________________                                    

Lactobacillus Evaluation

An evaluation of a prior art corn gluten feed dried to the usualmoisture content of less than 10% disclosed a Lactobacillus count of35/g compared with a count of 1350/gm for a high moisture content (50%by weight) wet corn bran/corn steep liquor product.

Evaluation of pH

All pH values given in this specification were obtained using thefollowing procedure:

10 g of animal feed product, or component thereof, was added to 100 mlof freshly boiled water (i.e. any dissolved CO₂ had been removed) themixture was allowed to stand for at least 30 minutes and the pH wasevaluated using a standard pH meter.

B. This plant is located in New York State and is larger than the plantreferred to in A. The corn steep liquor was concentrated in the usualmanner and the wet corn bran stream concentrated mechanically as in A.

(i) The two starting components had the following compositions:

    ______________________________________                                                    (a) Dry Matter                                                                          (b) Crude Protein                                       ______________________________________                                        Corn Steep Liquor                                                                           52.1        39.5                                                Wet Corn Bran 40.8        27.0                                                ______________________________________                                         Note:                                                                         The moisture content of the wet corn bran was 59.2 which, a indicated         previously, is significantly higher than normal.                         

A batch consisting of approximately 33,660 lbs of the desiredunfermented product was formed by mixing, over a period of 45 minutes13,370 lbs. of corn steep and 20,290 lbs. of wet corn bran i.e. theratio of the ratio of corn/bran:corn steep liquor being 1.51.:1.0. Theresulting unfermented feed supplement was in the form of a cohesive masshaving the following composition:

    ______________________________________                                        Dry Matter      38.9%                                                         Crude Protein   27.0%                                                         pH              3.85                                                          Bulk Density    57.2 lbs/cuft.                                                ______________________________________                                    

The product was shipped by truck directly to the consumer whereconstituted several weeks supply of protein supplement for a dairy herd.Both the unfermented and fermented products of the invention whichresulted from this batch performed perfectly satisfactorily.

(ii) Thw two starting components had the following composition:

    ______________________________________                                                    (a) Dry Matter                                                                          (b) Crude Protein                                       ______________________________________                                        Corn Steep Liquor                                                                           52.1        39.5                                                Wet Corn Bran 40.8        12.8                                                ______________________________________                                         Note:                                                                         The moisture content of the wet corn bran was 50.2 which is significantly     more than that of wet corn bran usually emanating from a wet corn milling     operation.                                                               

A batch of approximately 33,460 lbs of the desired unfermented productwas formed by thoroughing mixing on a continuous basis 11,370 lbs. ofthe corn steep liquor and 20,566 lbs. of the wet corn bran over a periodof 55 minutes, the ratio of wet corn bran:corn steep being 1.74:1. Theproduct was loaded into a truck and immediately transported to thecustomer. The unfermented feed supplement was in the form of a moistcohesive mass having the following composition:

    ______________________________________                                        Dry Matter       38.9%                                                        Crude Protein   26.9                                                          pH              3.61                                                          Bulk Density    5.72 lbs/cuft.                                                ______________________________________                                    

The above batch constituted a 2-3 week supply for the dairy herd inquestion. Feeding comenced virtually immediately upon delivery andconsequently, a portion of the feed supplement was utilized in theunfermented condition and the remainder, which remained in a undisturbedcondition, was used in the fermented condition.

(iii) The starting components had the following composition:

    ______________________________________                                                    (a) Dry Matter                                                                          (b) Crude Protein                                       ______________________________________                                        Corn Steep Liquor                                                                           47.6        42.9                                                Wet Corn Bran 39.8        13.1                                                ______________________________________                                         Note:                                                                         Again, the relatively high moisture content of the corn wet bran should b     noted.                                                                   

A batch of approximately 33,560 lbs. of the desired unfermented productwas produced by thoroughly mixing 12,678 lbs. of the corn steep liquorwith 21,482 lbs. of the dewatered wet corn bran. The ratio wet cornbran:corn steep liquor was 1.77:1 Product was produced over a period of60 minutes and loaded directly into a truck and immediately shipped tothe customer, owner of a dairy herd. The unfermented product in theusual form of a moist cohesive mass had the following composition:

    ______________________________________                                        Dry Matter      40.5%                                                         Crude Protein   25.7%                                                         pH              3.61                                                          Bulk Density    53.7                                                          ______________________________________                                    

The batch constituted a 2-3 week supply for the here. As previously,both unfermented and fermented products of the invention were utilizedas and when required with no adverse affects whatsoever.

All the products described in (i) (ii) and (iii) above had aLactobaccillus count in excess of 1000/gm.

The products described in (i) to (iii) above were commercial batches ofproducts of the invention and representative of batches supplied on acontinuous basis to customers. In most instances, the said products wereselected for use in the animal diets by way of a "least cost" computerprogram system, the said protein supplements being selected overalternatives such as corn and soya bean meal thus confirming the costeffectiveness as well as nutritional and practical effectiveness of theproducts of the invention. Moreover, it should be noted that all the wetcorn bran and the corn steep liquor emanating from the wet corn millingplant were utilized, as formed, in the practicing of the presentinvention. In other words, the rate of production of the animal feedsupplement is easily variable to conform with the plant when operatingat its greatest efficiency--a significant advantage.

FEEDING TRIALS

In feeding trials involving feeding Holstein steers (i.e. beef cattle),the product of the present invention, both unfermented and fermentedindiscriminately, was found to be an excellent supplemental proteinsource for high corn silage diets. The trial involved a comparison withother protein supplements and the results in summary form are given inthe following table:

    ______________________________________                                        Feeding Holstein Steers: Trial 5. Value of Wet Corn Gluten Feed                                        Roasted                                                        Urea Raw Beans Beans    Corn Gluten                                 ______________________________________                                        Initial Weight, lb.                                                                       209    202       205    198                                       Current Weight, lb.                                                                       544    617       656    651                                       Daily gain, lb.                                                                           1.86   2.31      2.51   2.52                                      ______________________________________                                    

As can be seen, the product of the present invention, termed "corngluten" in the table, compared very favourably with competitive productsand also has advantages from the viewpoint of cost. The products weretypical products obtained using the detailed processes desribedimmediately above in procedures (i) to (iii). For example, two typicalbatches had a dry matter values of 37.5 and 43.7 and crude proteinvalues of 23.0% and 23.5% respectively and met the given criteria forother essential parameters such as bulk density etc. The product wasdelivered from the same plant to the use site on a batch basis, onebatch every 2 to 3 weeks.

The embodiment of the invention in which an exclusive property orprivilege is claimed are defined as follows:
 1. A process for producinga moist, cohesive, friable, readily transportable animal feed supplementfrom wet corn bran and corn steep liquor exiting a wet corn millingprocess consisting essentially of:(a) mechanically de-watering the wetcorn bran to a solids content of from 30% to 50% by weight; (b)thoroughly admixing the de-watered bran with concentrated corn steepliquor having a solids content of from 40% to 55% by weight in a ratioof de-watered corn bran:concentrated corn steep liquor of from 3:1 to1:2, the resulting mixture having a solids content of from 35% to 50% byweight; and (c) compacting the resulting mixture to form a moist,cohesive, friable, readily transportable mass having a bulk density offrom 50 to 65 lb/cuft, a pH of less than 4.5 and a protein content of atleast 20% on a dry matter basis said animal feed supplement havingstorage stability for a period of time from two weeks to seven months.2. A process according to claim 1 wherein the pH of the moist cohesivemass of step (c) is from 3.50 to 4.2.
 3. A process according to claim 1or 2 wherein the mass produced in step (c) contains lactobacillusmicroorganisms in the amount of at least 1000/gm.
 4. A process accordingto claim 1 or 2 wherein the moist cohesive mass of step (c) has aprotein content of from 20% to 30% and a pH of from 3.5 to 4.1.
 5. Aprocess according to claim 1 or 2 wherein the wet corn bran isde-watered to a solids content of from 35% to 45%; the corn steep liquorhas a solids content of from 45% to 50% and the said two components aremixed in a ratio of from 3:1 to 1:1; and the moist cohesive mass has asolids content of from 38% to 42%, and a protein content of 22-25%.
 6. Aprocess for producing a moist, cohesive, friable, readily transportablemicrobiologically stable fermented animal feed supplement from wet cornbran and corn steep liquor exiting a wet corn milling process consistingessentially of:(a) mechanically de-watering the wet corn bran to asolids content of from 30% to 50% by weight; (b) thoroughly admixing thede-watered bran with concentrated corn steep liquor having a solidscontent of from 45% to 55% by weight in the ratio of de-watered cornbran:concentrated corn steep liquor or from 3:1 to 1:1 and the resultingmixture has a solids content of from 35% to 50% by weight; (c)compacting the resulting mixture to form a moist, cohesive, friable,readily transportable mass having a bulk density of from 50 to 65lb/cuft, a pH of less than 4.5 and a protein content of at least 20% ona dry matter basis; and (d) permitting said compacted moist cohesivemass to subsequently undergo a natural fermentation in a substantiallyanaerobic condition, said mass having a pH of less than 4.25 which massis gravitationally and microbiologically stable for a period of timefrom two weeks to seven months and readily reduced to anon-agglomerating product.
 7. A process according to claim 6 whereinsaid fermentation lasts for a period of at least seven (7) days.
 8. Aprocess according to claim 6 or 7 wherein the moist cohesive mass ofstep (c) has a pH of from 3.50 to 4.2.
 9. A process according to claim 6or 7 wherein the moist cohesive mass of step (c) has a protein contentof from 20% to 30% and a pH of from 3.5 to 4.1.
 10. A process accordingto claim 6 or 7 wherein a product of step (d) has a lactobacillusmicroorganism content of at least 1000/gm.
 11. In a wet corn millingprocess wherein wet corn bran is dewatered to increase its solidscontent before drying with heat and wherein concentrated corn steepliquor is a by-product of said process, the improvement consistingessentially of mixing said dewatered bran with said concentrated cornsteep liquor in a ratio of about 3:1 to about 1:2 to provide a moist,cohesive, friable, readily transportable animal feed supplement having asolids content of about 35 to about 50 weight % whereby the need to drysaid dewatered wet corn bran with heat is eliminated and whereby saidanimal feed supplement is resistant to microbial degradation for aperiod of time from two weeks to seven months.